tube rupture and other terminologies in chemical engineering
TRANSCRIPT
Table of contentsTube Rupture
◦ Line of action…………………………………………..
◦ Why it occurs…………………………………………..
◦ Stages………………………………………………….....
◦ How to avoid…………………………………………..
Battery Limits:◦ Usage in industries………………………………..◦ Pictorial representation…………………………
Personal protective equipment
◦ Types of Hazard………………………………….
Air Sox
Tube Rupture
When a tube breaks down due to conditions that are considered haphazard, such a definition is known as tube rupture. It can be defined in two ways
a) The tube failure is a sharp break in one tube.
b) The tube failure is assumed to occur at the back side of the tube sheet.
1. When there is a significant pressure differencebetween the shell and tube side of the heatexchanger
2. When the high pressure zone exceeds a pressure of1000psig
3. If the high pressure side contains a liquid or a vapor,that may vaporize and can result in the subsequentvaporization of the liquid on low pressure zone.
2/3rd rule
It states that:
◦ If pressure on the low pressure side is greater than or equal to 2/3rd of the pressure on the high pressure side, there is negligible danger of tube rupture
10/13 rule
It states that:◦ If pressure on the low pressure side is greater than
or equal to 10/13 on the high pressure side, then the risk of tube rupture can be ignored
Hydro-static testThis test is basically used to minimize the tube rupture characteristic of the pipe.
It is carried out before the tube or pipe is used in a setting i.e. that of heat exchanger.
It is used to test pipelines, gas cylinders, boilers for strength and leaks
1. The tube is filled with a incompressible liquid i.e. water
2. One side is closed while water is filled through other side
3. Pressure is increased above the design pressure
4. After Pressure is achieved, supply valve is closed and Pressure monitored
5. If there is a decrease in Pressure, it will indicate some sort of leakage
6. By doing this, we can determine leakage, strength and location of leakage
Steps1. Analysis of the heat exchanger should be carried out
considering the tube vibration, tube wall thickness.
2. Usage of PSV’s
3. The design pressure of the heat exchanger should be increased if it is operated at high pressure in order to mitigate tube rupture
4. If possible, it is best to keep the low pressure fluid on the shell side.
5. Usage of a vapor pocket on low pressure side
Battery LimitAreas which are specifically designated to different departments in a refinery or a chemical plant is known as battery limit.
This is more often than not, a physical boundary, that is used to differentiate the process units from the supporting equipment
Battery limits help to define the role of an engineer by making him know that which task he is expected to do, in which area of the industry
Personal Protective equipment
Personal protective equipment's or PPE’s, are the devices thatare used for safety not only in the industries, but everywhere.
Since the introduction of safety standards i.e. OHSAS, PPE’s havebecome an integral part of modern industries.
Their basic purpose is to reduce the hazards to which, theemployees will be exposed in engineering works
Regulations:
1. Properly assessed before usage to make sure it is suitable for the purpose
2. Maintained and stored properly
3. Provided with instructions on how to use it safely
4. Used correctly by employees
Limitations:
1. discrepancy between theoretical and actual levels of protection provided exists
2. only effective if correctly selected, fitted, used, and cared for, and the individual is trained.
3. the choice of PPE may compromise mobility, visibility, communication
Air SoxAir Sox, or in common language known as wind sox, are used to determine the direction of air flow.
It is designed to indicate wind direction and wind speed.
Wind-speed is indicated by the wind-sox’ angle relative to the mounting pole.
They are typically used at gas plants and airports